In this simulation, a degree-of-freedom analysis is performed on a distillation process to
determine whether the system has sufficient information to solve for the unknown variables. Use
buttons to select the unit on which to do mass balances (distillation column, condenser, or
reboiler) or to do a balance on the overall system. When “condenser” is selected, use buttons to
select “partial condenser” or “total condenser”. Set the “total number of unknowns” with the
slider; unknown variables are colored blue on the diagram and known variables are black. The
known variables are selected randomly, and they change when you click the “new problem” button.
Use buttons to select how species B is represented: as zB or as 1 – zA;
the degree-of-freedom
analysis is different for each representation. An explanation of the analysis is shown on the
right. For zero degrees of freedom, the balances are solvable. The system is overspecified if it
has more equations than unknowns and it is underspecified if it has more unknowns than
equations. For a reboiler, the equilibrium ratio Kr, is known, and for a partial
condenser the
equilibrium ratio Kc is known. Temperatures and pressures are known for this
analysis. Mass
balances and phase equilibrium relations are solved to determine the unknown variables.